EP0565403A1 - Silica/acrylation dispersions, method for producing them, their use in stereophotolithography and method for preparing articles made of resin - Google Patents
Silica/acrylation dispersions, method for producing them, their use in stereophotolithography and method for preparing articles made of resin Download PDFInfo
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- EP0565403A1 EP0565403A1 EP93400805A EP93400805A EP0565403A1 EP 0565403 A1 EP0565403 A1 EP 0565403A1 EP 93400805 A EP93400805 A EP 93400805A EP 93400805 A EP93400805 A EP 93400805A EP 0565403 A1 EP0565403 A1 EP 0565403A1
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- Prior art keywords
- silica
- weight
- average diameter
- particles
- dispersions
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/113—Silicon oxides; Hydrates thereof
- C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
- C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
- C01B33/145—Preparation of hydroorganosols, organosols or dispersions in an organic medium
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- G—PHYSICS
- G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
- G03F—PHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
- G03F7/00—Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
- G03F7/0037—Production of three-dimensional images
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- G—PHYSICS
- G03—PHOTOGRAPHY; CINEMATOGRAPHY; ANALOGOUS TECHNIQUES USING WAVES OTHER THAN OPTICAL WAVES; ELECTROGRAPHY; HOLOGRAPHY
- G03F—PHOTOMECHANICAL PRODUCTION OF TEXTURED OR PATTERNED SURFACES, e.g. FOR PRINTING, FOR PROCESSING OF SEMICONDUCTOR DEVICES; MATERIALS THEREFOR; ORIGINALS THEREFOR; APPARATUS SPECIALLY ADAPTED THEREFOR
- G03F7/00—Photomechanical, e.g. photolithographic, production of textured or patterned surfaces, e.g. printing surfaces; Materials therefor, e.g. comprising photoresists; Apparatus specially adapted therefor
- G03F7/004—Photosensitive materials
- G03F7/075—Silicon-containing compounds
Definitions
- the present invention relates to silicone-acrylic dispersions, their production process, their application in stereophotolithography and a process for the preparation of resin objects.
- Stereophotolithography is nowadays more and more used to manufacture complex parts of small dimensions, from photosensitive resins.
- the resins currently available on the market for this technique do not yet make it possible to obtain objects meeting all the requirements of the user who wishes to have available, at low cost, reliable objects, of good presentation, having excellent mechanical properties and correct aging.
- Dispersions of colloidal silica in 2-hydroxyethyl acrylate are already known, but to the knowledge of the applicant, these silica dispersions, on the one hand, are monodispersed, that is to say that the dispersed silica particles have substantially all of the same average diameter, and on the other hand they contain by weight less than 50% of silica.
- dispersions are easily obtained by mixing, at room temperature, a monodisperse silica hydrosol, in acid form, containing less than 50% by weight of colloidal silica, including the discrete silica particles, not linked together by siloxane bonds, have an identical average diameter of between 10 and 50 nm, with 2-hydroxyethyl acrylate, then removing the water from this mixture, usually by azeotropic distillation under reduced pressure, until obtaining an organosol of silica practically free of water and containing by weight less than 50% of silica.
- the present invention relates to dispersions of colloidal silica in an alkanol acrylate, or a mixture of alkanol acrylates, of general formula (I).
- R and R 1 ′ identical represent a hydrogen atom
- R and R 1 ′ different represent a hydrogen atom or a methyl radical, characterized in that they contain by weight from 50 to 70 % silica in the form of discrete, polydisperse particles, not linked to each other by siloxane bonds with an average diameter of between 10 and 50 nm.
- polydisperses is meant that the study of the dispersion of the particles indicates the existence of several peaks, therefore corresponding to several mean diameters.
- the subject of the invention is in particular dispersions characterized by the fact that 20 to 50% by weight of the silica present is in the form of discrete particles, of an identical average diameter, less than or equal to half the average diameter of at least 50% by weight of the remaining silica particles.
- the subject of the invention is in particular a dispersion of colloidal silica dispersed in 2-hydroxyethyl acrylate containing 50 to 70% by weight of silica in the form of discrete particles not linked together by siloxane bonds, having for 40 to 50% by weight of them an average diameter of approximately 13 nm, and for the complement to 100%, an average diameter of approximately 50 nm.
- the alkanol acrylates of general formula (I) are either, and preferably 2-hydroxyethyl acrylate, or a mixture in variable proportions of the monoesters of acrylic acid with propanediol-1,2. These monomers are known and they are marketed stabilized with from 0.1 to 0.01% by weight of a stabilizer such as paramethoxyphenol. This stabilizer is kept in the dispersions of the present invention, when using such commercial products.
- the invention particularly relates to the dispersions of colloidal silica described in the examples.
- the present application also relates to a process for the preparation of the above dispersions, characterized in that a silica hydrosol, monodisperse, in acid form, containing 30 to 30% by weight, is mixed, with stirring 50% silica in the form of discrete particles not linked to each other by siloxane bonds, with an average diameter of 10 to 50 nm with a calculated amount of an alkanol acrylate or a mixture of acrylate d alkanol of general formula (I) above so as to obtain the desired silica content of between 50 and 70% by weight, then distilling the water present in this dispersion, at a temperature below 55 ° C, under reduced pressure and with stirring, to a residual water content of less than 1% by weight, determined by the Karl Fischer method, to obtain a monodisperse dispersion of colloidal silica in alkanol acrylate, or the mixture of alkano acrylates ls of general formula (I) chosen, containing from 50 to 70% by weight of silica in the form of
- the present application relates in particular to the above process, characterized in that a monodisperse dispersion of colloidal silica particles of a certain diameter is prepared, which is mixed with at least one monodisperse dispersion of colloidal silica particles with an average diameter less than or equal to half the average diameter of the first silica particles, the last silica particles representing 20 to 50% by weight of the silica present, while the first silica particles represent at least 50% of the remaining silica particles.
- a dispersion according to the present invention containing 2-hydroxyethyl acrylate 62.5% of silica in the form of discrete particles having, for 48% by weight of them, an average diameter of 13 nm and for the complement to 100%, an average diameter of 50 nm
- identical quantities of a dispersion of colloidal monodisperse silica in 2-hydroxyethyl acrylate containing 60% are mixed at room temperature.
- the present invention also relates to dispersions of colloidal silica obtained by the above methods.
- silica hydrosols monodisperse, in acid form
- the silica hydrosols, monodisperse, in acid form are obtained by known methods, in particular by leaching of the corresponding commercial silica hydrosol stabilized by an alkaline agent, such as ammonia or an alkali metal hydroxide on a bed of cation exchange resin in acid form.
- an alkaline agent such as ammonia or an alkali metal hydroxide
- KLEBOSOL R by the French Company Hoechst.
- the silico-acrylic dispersions according to the present invention can be either diluted in all proportions with an alkanol acrylate of general formula (I), to reduce, if desired, their silica concentration, or concentrated under reduced pressure and with stirring, at a temperature below 55 ° C, to raise, if desired, their silica concentration up to 70% by weight.
- an alkanol acrylate of general formula (I) to reduce, if desired, their silica concentration, or concentrated under reduced pressure and with stirring, at a temperature below 55 ° C, to raise, if desired, their silica concentration up to 70% by weight.
- the silica content of the silico-acrylic dispersions according to the present invention is determined by calcination of a sample of known weight.
- the particle size it can be determined by transmission electron microscopy or, indirectly, by nitrogen adsorption after drying of the dispersion according to S. Brunauer et al., J. Amer, Chem. Soc., 60, 309 (1938).
- the silico-acrylic dispersions according to the present invention have interesting properties in stereophotolithography.
- photosensitive polymerization initiators commonly designated photoinitiators
- a derivative of a substituted aromatic ketone such as benzophenone, 1-hydroxy cyclohexylphenyl ketone, 2-methyl-2-morpholino paramethylthiopropiophenone.
- Various conventional additives can also be introduced for this type of application, such as a polymerization inhibitor such as paramethoxyphenol, hydroquinone, a co-initiator, a dispersant, dyes and / or pigments.
- the total weight of the additives introduced is less than 10% by weight of the dispersion.
- the level of one or more radical polymerization inhibitors such as paramethoxyphenol or hydroquinone is supplemented, up to 2% by weight, this avoids parasitic polymerizations , and in particular, those induced by the light scattered by the silica particles during their irradiation using an active laser beam.
- photosensitive polymerization initiator (s) with one or more thermal polymerization initiators such as benzoyl peroxide when using a thermal laser of the C0 2 type in SPL.
- thermal polymerization initiators such as benzoyl peroxide
- the photosensitive or thermal initiator (s) used, as well as the various additives, are generally introduced into the dispersions according to the present invention, just before their use in stereophotolithography.
- one or more radical polymerization inhibitors such as paramethoxyphenol, or hydroquinone are present during their preparation.
- the dispersions according to the present invention have interesting properties, and in particular they lead during and after the polymerization induced with a laser beam, to very low volume shrinkages.
- volume shrinkage by relation (1): in which dm and dp represent respectively the density of the monomer and of the polymerized monomer. These densities are determined by conventional methods.
- a thin layer of a dispersion according to the pre is deposited on a dish suspended with wires on a pan of a precision balance. invention, containing 2% by weight of 2-methyl-2-morpholino paramethylthiopropiophenone.
- the cup is completely immersed in paraffin oil of density 0.86.
- the difference in the masses of the sample in air and in paraffin oil makes it possible to know its volume.
- the sample in the paraffin oil is then irradiated with a UV light beam, it polymerizes slowly.
- the mass of the sample in the paraffin oil varies as a function of the variation in its volume during the polymerization.
- the same experiment is carried out in the absence of monomer and the values obtained are subtracted from the experimental values found with the sample.
- the volume shrinkage is calculated using the relation (1), then the graph of the volume shrinkage thus calculated is constructed as a function of the polymerization time. It is thus found that with the dispersions according to the present invention, the shrinkage is zero at the start of polymerization, then it increases regularly as a function of time, up to a limit value identical to the value found directly on the polymer by application of the relation (1).
- the dispersions according to the present invention also have a good depth of polymerization. This characteristic is an important factor for obtaining objects in stereophotolithography, because a too low polymerization depth does not allow satisfactory adhesion of the layers. Furthermore, due to their good transparency properties, the dispersions according to the invention diffuse little active light, which results in good spatial resolution.
- IRGATURE R 500 which is an equal-weight mixture of benzophenone and, is placed in a tank for UV spectrophotometer, of section 1 cm 2 .
- 1-hydroxy-cyclohexylphenyl ketone then the sample is punctually irradiated with a laser beam for a determined period (1 minute for a laser with a power of 100 mW).
- the tank is then emptied, the polymer obtained is washed with acetone, then the height of the peak of the polymer formed at the point of impact of the laser beam is measured.
- the heights of the peaks measured vary from 4 to 7 mm, corresponding to a very good depth of polymerization.
- the dispersions according to the present invention also have a satisfactory viscosity for producing objects of complex shape in stereophotolithography without problem.
- 8000 g of a silica hydrosol sold under the name of KLEBOSOL R 1344 Na by the French company Hoechst are mixed at ambient temperature, with stirring, having a pH of 9.7 and containing 69.6% by weight of water, 0.4% Na 2 0 and 30% silica in the form of monodisperse particles, not linked to each other by siloxane bonds and having an average diameter of 13 nm with 708 g (0.9 I) of a resin cation exchanger with sulfonic groups in acid form and with an exchange capacity of 2 eq / 1.
- 2110 g of a silica organosol are thus obtained containing by weight 38.4% of 2-hydroxyethyl acrylate, 0.6% of water determined by the Karl Fischer method, 0.8% of hydroquinone and 60.2% silica in the form of discrete, monodisperse particles, with an average diameter of 13 nm, not linked to each other by siloxane bonds and having at 20 ° C, a density of 1.576 and a Brookfield viscosity of 2200 mPa.s at 780 rpm.
- a silicone-acrylic dispersion containing 30.3% by weight of acrylate of 2-hydroxyethyl, 0.8% of hydroquinone, 0.7% of water and 68.2% of silica in the form of discrete, monodisperse particles, with an average diameter of 50 nm, unbound between them by siloxane bonds, and having a Brookfield viscosity, determined at 20 ° C., at 780 rpm of 8000 mPa.s.
- This silico-acrylic dispersion is then diluted with 100 g of 2-hydroxyethyl acrylate to bring its silica titer to 65% by weight.
- a silicone-acrylic dispersion is thus obtained having, at 20 ° C., a density of 1.635 and a Brookfield viscosity of 740 mPa.s, at 780 rpm and containing by weight 33.5% of hydroxy acrylate. 2 ethyl, 0.7% water, 0.8% hydroquinone and 65% silica in the form of monodisperse particles with an average diameter of 50 nm, not linked to each other by siloxane bonds.
- 500 g of the silica-acrylic dispersion obtained in Example 1 and 500 g of the silico-acrylic dispersion obtained in Example 2 are mixed with stirring at room temperature. 1000 g of a silico dispersion are thus obtained -acrylic containing 36% by weight of 2-hydroxyethyl acrylate, 0.7% of water, 0.7% of hydroquinone and 62.5% of silica in the form of discrete, polydisperse, unbound particles between them by siloxane bonds, 48% of which by weight, have an average diameter of 13 nm and 52% an average diameter of 50 nm.
- This dispersion has a density of 1.605.
- silica acid hydrosol prepared in Example 1 666.7 g of the silica acid hydrosol prepared in Example 1 are mixed with room temperature, with stirring, with 200 g of a mixture of acrylic acid monoester with 1,2-propanediol containing 75 % of 2-hydroxypropyl acrylate, 25% of 2-hydroxyethyl methyl-1 ethyl acrylate and 33.4 g of hydroquinone. Then, the water present in this reaction medium is distilled, with stirring, at a temperature below 55 ° C, under a pressure gradually reduced from 60 to 20 mbar.
- 400 g of a silico-acrylic dispersion are thus obtained, containing by weight 48% of monoesters of acrylic acid with propanediol-1,2, 0.8% of hydroquinone, 0.8% of water and 50% of silica in the state of monodisperse particles, with an average diameter of 13 nm, not linked to each other by siloxane bonds and having at 20 ° C, a density of 1.446 and a Brookfield viscosity, at 780 rpm, of 1528 mPa.s.
- a honeycomb cube is prepared, as in Example 5, with the dispersions prepared in Examples 1 and 2 into which 1% by weight of benzophenone and 1% by weight of 1-hydroxycyclohexylphenylketone have been introduced. This gives two honeycomb cubes of correct presentation, with transparent and well-defined walls.
- the volume shrinkage is 6% for the dispersion of Example 1 and 1.5% for the dispersion of Example 2.
- a honeycomb cube is prepared as in Example 5 after introduction into the dispersion of 1% by weight of benzophenone and 1% by weight of 1-hydroxy cyclohexylphenyl ketone.
Abstract
Description
La présente invention concerne des dispersions silico-acryliques, leur procédé d'obtention, leur application en stéréophotolithographie et un procédé de préparation d'objets en résine.The present invention relates to silicone-acrylic dispersions, their production process, their application in stereophotolithography and a process for the preparation of resin objects.
La stéréophotolithographie est actuellement de plus en plus utilisée pour fabriquer des pièces complexes de petites dimensions, à partir de résines photosensibles. Les résines actuellement disponibles sur le marché pour cette technique, ne permettent pas encore d'obtenir des objets répondant à toutes les exigences de l'utilisateur qui souhaite disposer, à faible prix, d'objets fiables, de bonne présentation, possédant d'excellentes propriétés mécaniques et un vieillissement correct.Stereophotolithography is nowadays more and more used to manufacture complex parts of small dimensions, from photosensitive resins. The resins currently available on the market for this technique do not yet make it possible to obtain objects meeting all the requirements of the user who wishes to have available, at low cost, reliable objects, of good presentation, having excellent mechanical properties and correct aging.
Afin de répondre à cette demande, la demanderesse a découvert avec étonnement que certaines dispersions de silice colloïdale présentent d'excellentes propriétés applicatives en stéréophotolithographie.In order to respond to this request, the applicant has discovered with astonishment that certain dispersions of colloidal silica have excellent application properties in stereophotolithography.
On connaît déjà des dispersions de silice colloïdale dans l'acrylate d'hydroxy-2 éthyle, mais à la connaissance de la demanderesse, ces dispersions de silice, d'une part sont monodisperses c'est à dire que les particules de silice dispersées présentent sensiblement toutes un même diamètre moyen, et d'autre part elles contiennent pondéralement moins de 50% de silice. Ces dispersions sont aisément obtenues en mélangeant, à la température ambiante, un hydrosol de silice monodisperse, sous forme acide, contenant moins de 50% en poids de silice colloïdale, dont les particules discrètes de silice, non liées entre elles par des liaisons siloxane, présentent un diamètre moyen identique compris entre 10 et 50 nm, avec de l'acrylate d'hydroxy-2 éthyle, puis en éliminant l'eau de ce mélange, habituellement par distillation azéotropique sous pression réduite, jusqu'à l'obtention d'un organosol de silice pratiquement exempt d'eau et contenant pondéralement moins de 50% de silice.Dispersions of colloidal silica in 2-hydroxyethyl acrylate are already known, but to the knowledge of the applicant, these silica dispersions, on the one hand, are monodispersed, that is to say that the dispersed silica particles have substantially all of the same average diameter, and on the other hand they contain by weight less than 50% of silica. These dispersions are easily obtained by mixing, at room temperature, a monodisperse silica hydrosol, in acid form, containing less than 50% by weight of colloidal silica, including the discrete silica particles, not linked together by siloxane bonds, have an identical average diameter of between 10 and 50 nm, with 2-hydroxyethyl acrylate, then removing the water from this mixture, usually by azeotropic distillation under reduced pressure, until obtaining an organosol of silica practically free of water and containing by weight less than 50% of silica.
C'est pourquoi la présente invention a pour objet des dispersions de silice colloïdale dans un acrylate d'alcanol, ou un mélange d'acrylates d'alcanols, de formule générale (I).
dans laquelle soit R et R1' identiques, représentent un atome d'hydrogène, soit R et R1' différents, représentent, un atome d'hydrogène ou un radical méthyle, caractérisées par le fait qu'elles contiennent pondéralement de 50 à 70% de silice à l'état de particules discrètes, polydisperses, non liées entre elles par des liaisons siloxane d'un diamètre moyen compris entre 10 et 50 nm.This is why the present invention relates to dispersions of colloidal silica in an alkanol acrylate, or a mixture of alkanol acrylates, of general formula (I).
in which either R and R 1 ′ identical represent a hydrogen atom, or R and R 1 ′ different represent a hydrogen atom or a methyl radical, characterized in that they contain by weight from 50 to 70 % silica in the form of discrete, polydisperse particles, not linked to each other by siloxane bonds with an average diameter of between 10 and 50 nm.
Par "polydisperses", l'on entend que l'étude de la dispersion des particules indique l'existence de plusieurs pics, correspondant donc à plusieurs diamètres moyens.By "polydisperses" is meant that the study of the dispersion of the particles indicates the existence of several peaks, therefore corresponding to several mean diameters.
Parmi ces dispersions, l'invention a notamment pour objet des dispersions caractérisées par le fait
que 20 à 50% en poids de la silice présente est sous forme de particules discrètes, d'un diamètre moyen identique, inférieur ou égal à la moitié du diamètre moyen d'au moins 50% en poids des particules de silice restantes.Among these dispersions, the subject of the invention is in particular dispersions characterized by the fact
that 20 to 50% by weight of the silica present is in the form of discrete particles, of an identical average diameter, less than or equal to half the average diameter of at least 50% by weight of the remaining silica particles.
Parmi ces dernières dispersions, l'invention a notamment pour objet une dispersion de silice colloïdale dispersée dans de l'acrylate d'hydroxy-2 éthyle contenant pondéralement de 50 à 70 % de silice à l'état de particules discrètes non liées entre elles par des liaisons siloxane, présentant pour 40 à 50 % en poids d'entre elles un diamètre moyen d'environ 13 nm, et pour le complément à 100 %, un diamètre moyen d'environ de 50 nm.Among these latter dispersions, the subject of the invention is in particular a dispersion of colloidal silica dispersed in 2-hydroxyethyl acrylate containing 50 to 70% by weight of silica in the form of discrete particles not linked together by siloxane bonds, having for 40 to 50% by weight of them an average diameter of approximately 13 nm, and for the complement to 100%, an average diameter of approximately 50 nm.
Les acrylates d'alcanols de formule générale (I) sont soit, et de préférence l'acrylate d'hydroxy-2 éthyle, soit un mélange en proportions variables des monoesters de l'acide acrylique avec le propanediol-1,2. Ces monomères sont connus et ils sont commercialisés stabilisés avec de 0,1 à 0,01 % en poids d'un stabilisant tel que le paraméthoxyphénol. Ce stabilisant est conservé dans les dispersions de la présente invention, en cas d'utilisation des tels produits commerciaux.The alkanol acrylates of general formula (I) are either, and preferably 2-hydroxyethyl acrylate, or a mixture in variable proportions of the monoesters of acrylic acid with propanediol-1,2. These monomers are known and they are marketed stabilized with from 0.1 to 0.01% by weight of a stabilizer such as paramethoxyphenol. This stabilizer is kept in the dispersions of the present invention, when using such commercial products.
L'invention a tout particulièrement pour objet les dispersions de silice colloïdale décrites dans les exemples.The invention particularly relates to the dispersions of colloidal silica described in the examples.
La présente demande a aussi pour objet un procédé de préparation des dispersions ci-dessus, caractérisé par le fait que l'on mélange, sous agitation, à la température ambiante, un hydrosol de silice, monodisperse, sous forme acide, contenant pondéralement 30 à 50 % de silice à l'état de particules discrètes non liées entre elles par des liaisons siloxane, d'un diamètre moyen de 10 à 50 nm avec une quantité calculée d'un acrylate d'alcanol ou d'un mélange d'acrylate d'alcanol de formule générale (I) ci-dessus de manière à obtenir le taux de silice désiré compris entre 50 et 70 % en poids, puis que l'on distille l'eau présente dans cette dispersion, à une température inférieure à 55°C, sous pression réduite et sous agitation, jusqu'à un taux d'eau résiduelle inférieur à 1 % en poids, déterminé par la méthode de Karl Fischer, pour obtenir une dispersion monodisperse de silice colloïdale dans l'acrylate d'alcanol, ou le mélange d'acrylates d'alcanols de formule générale (I) choisi, contenant de 50 à 70 % en poids de silice sous forme de particules discrètes non liées entre elles par des liaisons siloxane, présentant un diamètre moyen de 10 à 50 nm que l'on isole ou, si désiré l'on mélange, à la température ambiante, dans des proportions convenables, avec une ou plusieurs autres dispersions monodisperses de silice colloïdale de granulométrie souhaitée et de taux de silice adéquat, dans un acrylate d'alcanol, ou un mélange d'acrylates d'alca- nols de formule générale (I) identique et préparées selon le procédé décrit ci-dessus, de manière à obtenir la dispersion silicoacrylique polydisperse souhaitée.The present application also relates to a process for the preparation of the above dispersions, characterized in that a silica hydrosol, monodisperse, in acid form, containing 30 to 30% by weight, is mixed, with stirring 50% silica in the form of discrete particles not linked to each other by siloxane bonds, with an average diameter of 10 to 50 nm with a calculated amount of an alkanol acrylate or a mixture of acrylate d alkanol of general formula (I) above so as to obtain the desired silica content of between 50 and 70% by weight, then distilling the water present in this dispersion, at a temperature below 55 ° C, under reduced pressure and with stirring, to a residual water content of less than 1% by weight, determined by the Karl Fischer method, to obtain a monodisperse dispersion of colloidal silica in alkanol acrylate, or the mixture of alkano acrylates ls of general formula (I) chosen, containing from 50 to 70% by weight of silica in the form of discrete particles not linked to each other by siloxane bonds, having an average diameter of 10 to 50 nm which are isolated or, if desired, it is mixed, at room temperature, in suitable proportions, with one or more other monodisperse dispersions of colloidal silica of desired particle size and adequate silica content, in an alkanol acrylate, or a mixture of acrylates of alkanols of general formula (I) identical and prepared according to the process described above, so as to obtain the desired polydisperse silicoacrylic dispersion tee.
La présente demande a notamment pour objet le procédé ci-dessus caractérisé par le fait que l'on prépare une dispersion monodisperse de particules de silice colloïdale d'un certain diamètre que l'on mélange avec au moins une dispersion monodisperse de particules de silice colloïdale d'un diamètre moyen inférieur ou égal à la moitié du diamètre moyen des premières particules de silice, les dernières particules de silice représentant 20 à 50 % en poids de la silice présente, tandis que les premières particules de silice représentent au moins 50 % des particules de silice restantes.The present application relates in particular to the above process, characterized in that a monodisperse dispersion of colloidal silica particles of a certain diameter is prepared, which is mixed with at least one monodisperse dispersion of colloidal silica particles with an average diameter less than or equal to half the average diameter of the first silica particles, the last silica particles representing 20 to 50% by weight of the silica present, while the first silica particles represent at least 50% of the remaining silica particles.
Elle a particulièrement pour objet le procédé ci-dessus caractérisé par le fait que 40 à 50 % en poids des particules de silice ont un diamètre moyen d'environ 13 nm, et le complément à 100 % a un diamètre moyen d'environ 50 nm.Its particular subject is the above process, characterized in that 40 to 50% by weight of the silica particles have an average diameter of approximately 13 nm, and the complement to 100% has an average diameter of approximately 50 nm .
Ainsi, pour obtenir une dispersion selon la présente invention contenant de l'acrylate d'hydroxy-2 éthyle, 62,5 % de silice à l'état de particules discrètes présentant pour 48 % en poids d'entre elles, un diamètre moyen de 13 nm et pour le complément à 100 %, un diamètre moyen de 50 nm, on mélange, à la température ambiante, des quantités identiques d'une dispersion de silice colloïdale monodisperse dans l'acrylate d'hydroxy-2 éthyle contenant 60 % en poids de silice à l'état de particules d'un diamètre moyen de 13 nm et d'une dispersion de silice colloïdale monodisperse dans l'acrylate d'hydroxy-2 éthyle contenant 65 % en poids de silice à l'état de particules d'un diamètre moyen de 50 nm.Thus, to obtain a dispersion according to the present invention containing 2-hydroxyethyl acrylate, 62.5% of silica in the form of discrete particles having, for 48% by weight of them, an average diameter of 13 nm and for the complement to 100%, an average diameter of 50 nm, identical quantities of a dispersion of colloidal monodisperse silica in 2-hydroxyethyl acrylate containing 60% are mixed at room temperature. weight of silica in the form of particles with an average diameter of 13 nm and of a dispersion of monodisperse colloidal silica in 2-hydroxyethyl acrylate containing 65% by weight of silica in the form of particles d '' an average diameter of 50 nm.
La présente invention a aussi pour objet des dispersions de silice colloïdale obtenues par les procédés ci-dessus.The present invention also relates to dispersions of colloidal silica obtained by the above methods.
Les hydrosols de silice, monodisperses, sous forme acide, sont obtenus par des procédés connus, notamment par lixiviation de l'hydrosol de silice correspondant commercial stabilisé par un agent alcalin, tel que l'ammoniaque ou un hydroxyde de métal alcalin sur un lit de résine échangeuse de cations sous forme acide. On peut citer par exemple ceux commercialisés sous les noms de KLEBOSOLR par la Société Française Hoechst.The silica hydrosols, monodisperse, in acid form, are obtained by known methods, in particular by leaching of the corresponding commercial silica hydrosol stabilized by an alkaline agent, such as ammonia or an alkali metal hydroxide on a bed of cation exchange resin in acid form. We can quote for example those marketed under the names of KLEBOSOL R by the French Company Hoechst.
Les dispersions silico-acryliques selon la présente invention peuvent être, soit diluées en toutes proportions avec un acrylate d'alcanol de formule générale (I), pour diminuer, si désiré, leur concentration en silice, soit concentrées sous pression réduite et sous agitation, à une température inférieure à 55°C, pour élever, si désiré, leur concentration en silice jusqu'à 70 % en poids.The silico-acrylic dispersions according to the present invention can be either diluted in all proportions with an alkanol acrylate of general formula (I), to reduce, if desired, their silica concentration, or concentrated under reduced pressure and with stirring, at a temperature below 55 ° C, to raise, if desired, their silica concentration up to 70% by weight.
Le taux de silice des dispersions silico-acryliques selon la présente invention, est déterminé par calcination d'un échantillon de poids connu. Quant à la granulométrie, elle peut être déterminée par microscopie électronique en transmission ou, indirectement, par adsorption d'azote après séchage de la dispersion selon S. Brunauer et al., J.Amer, Chem. Soc., 60, 309 (1938).The silica content of the silico-acrylic dispersions according to the present invention is determined by calcination of a sample of known weight. As for the particle size, it can be determined by transmission electron microscopy or, indirectly, by nitrogen adsorption after drying of the dispersion according to S. Brunauer et al., J. Amer, Chem. Soc., 60, 309 (1938).
Les dispersions silico-acryliques selon la présente invention présentent d'intéressantes propriétés en stéréophotolithographie.The silico-acrylic dispersions according to the present invention have interesting properties in stereophotolithography.
Pour leur application en stéréophotolithographie, on introduit par exemple dans les dispersions selon la présente invention, jusqu'à 5 % en poids d'un ou plusieurs amorceurs de polymérisation photosensibles désignés couramment photoamorceurs, tel qu'un dérivé d'une cétone aromatique substituée comme la benzophénone, l'hydroxy-1 cyclohexylphénylcétone, la méthyl-2 morpholino-2 paraméthylthiopropiophénone. On peut également introduire divers additifs classiques pour ce type d'application, tels qu'un inhibiteur de polymérisation comme le paraméthoxyphénol, l'hydroquinone, un co-amorceur, un dispersant, des colorants et/ou des pigments. Généralement, le poids total des additifs introduits est inférieur à 10% en poids de la dispersion. Avantageusement, dans les dispersions selon la présente invention destinées à la stéréophotolithographie, on complète le taux d'un ou plusieurs inhibiteurs de polymérisation radicalaire tels que le paraméthoxyphénol ou l'hydroquinone, jusqu'à 2 % en poids, on évite ainsi des polymérisations parasites, et notamment, celles induites parla lumière diffusée par les particules de silice lors de leur irradiation à l'aide d'un faisceau laser actif.For their application in stereophotolithography, up to 5% by weight of one or more photosensitive polymerization initiators commonly designated photoinitiators is introduced into the dispersions according to the present invention, such as a derivative of a substituted aromatic ketone such as benzophenone, 1-hydroxy cyclohexylphenyl ketone, 2-methyl-2-morpholino paramethylthiopropiophenone. Various conventional additives can also be introduced for this type of application, such as a polymerization inhibitor such as paramethoxyphenol, hydroquinone, a co-initiator, a dispersant, dyes and / or pigments. Generally, the total weight of the additives introduced is less than 10% by weight of the dispersion. Advantageously, in the dispersions according to the present invention intended for stereophotolithography, the level of one or more radical polymerization inhibitors such as paramethoxyphenol or hydroquinone is supplemented, up to 2% by weight, this avoids parasitic polymerizations , and in particular, those induced by the light scattered by the silica particles during their irradiation using an active laser beam.
Il est également possible de remplacer, partiellement ou totalement, le ou les amorceurs de polymérisation photosensibles par un ou plusieurs amorceurs de polymérisation thermiques tels que le peroxyde de benzoyle lorsque l'on utilise un laser thermique du type C02 en SPL.It is also possible to replace, partially or totally, the photosensitive polymerization initiator (s) with one or more thermal polymerization initiators such as benzoyl peroxide when using a thermal laser of the C0 2 type in SPL.
Le ou les amorceurs photosensibles ou thermiques utilisés, ainsi que les divers additifs, sont généralement introduits dans les dispersions selon la présente invention, juste avant leur utilisation en stéréophotolithographie. Toutefois, il est avantageux qu'un ou plusieurs inhibiteurs de polymérisation radicalaire tels que le paraméthoxyphénol, ou l'hydroquinone soient présents au cours de leur préparation.The photosensitive or thermal initiator (s) used, as well as the various additives, are generally introduced into the dispersions according to the present invention, just before their use in stereophotolithography. However, it is advantageous that one or more radical polymerization inhibitors such as paramethoxyphenol, or hydroquinone are present during their preparation.
En stéréophotolithographie, les dispersions selon la présente invention présentent d'intéressantes propriétés, et notamment elles conduisent pendant et après la polymérisation induite avec un faisceau laser, à de très faibles retraits volumiques.In stereophotolithography, the dispersions according to the present invention have interesting properties, and in particular they lead during and after the polymerization induced with a laser beam, to very low volume shrinkages.
On définit le retrait volumique par la relation (1) :
dans laquelle dm et dp représentent respectivement la masse volumique du monomère et du monomère polymérisé. Ces masses volumiques sont déterminées par les méthodes classiques.We define volume shrinkage by relation (1):
in which dm and dp represent respectively the density of the monomer and of the polymerized monomer. These densities are determined by conventional methods.
Pour connaître et étudier le retrait en cours de la polymérisation, on dépose sur une coupelle suspendue avec des fils à un plateau d'une balance de précision, une fine couche d'une dispersion selon la présente invention, contenant 2 % en poids de méthyl-2 morpholino-2 paraméthylthiopropiophénone. Après avoir noté la masse de l'échantillon, on immerge complètement la coupelle dans de l'huile de paraffine de densité 0,86. La différence des masses de l'échantillon dans l'air et dans l'huile de paraffine permet de connaître son volume. L'échantillon au sein de l'huile de paraffine est alors irradié avec un faisceau lumineux UV, il polymérise lentement. La masse de l'échantillon dans l'huile de paraffine varie en fonction de la variation de son volume au cours de la polymérisation. Parallèlement, on effectue la même expérience en l'absence de monomère et on retranche les valeurs obtenues des valeurs expérimentales trouvées avec l'échantillon.To know and study the shrinkage during the polymerization, a thin layer of a dispersion according to the pre is deposited on a dish suspended with wires on a pan of a precision balance. invention, containing 2% by weight of 2-methyl-2-morpholino paramethylthiopropiophenone. After having noted the mass of the sample, the cup is completely immersed in paraffin oil of density 0.86. The difference in the masses of the sample in air and in paraffin oil makes it possible to know its volume. The sample in the paraffin oil is then irradiated with a UV light beam, it polymerizes slowly. The mass of the sample in the paraffin oil varies as a function of the variation in its volume during the polymerization. At the same time, the same experiment is carried out in the absence of monomer and the values obtained are subtracted from the experimental values found with the sample.
Toutes les minutes, on calcule à l'aide de la relation (1) le retrait volumique, puis on construit le graphe du retrait volumique ainsi calculé en fonction du temps de polymérisation. On constate ainsi qu'avec les dispersions selon la présente invention, le retrait est nul en début de polymérisation, puis il croît régulièrement en fonction du temps, jusqu'à une valeur limite identique à la valeur trouvée directement sur le polymère par application de la relation (1).Every minute, the volume shrinkage is calculated using the relation (1), then the graph of the volume shrinkage thus calculated is constructed as a function of the polymerization time. It is thus found that with the dispersions according to the present invention, the shrinkage is zero at the start of polymerization, then it increases regularly as a function of time, up to a limit value identical to the value found directly on the polymer by application of the relation (1).
Les dispersions selon la présente invention présentent également un bonne profondeur de polymérisation. Cette caractéristique est un facteur important pour l'obtention d'objets en stéréophotolithographie, car une profondeur de polymérisation trop faible ne permet pas un accrochage satisfaisant des couches. Par ailleurs, de par leurs bonnes propriétés de transparence, les dispersions selon l'invention diffusent peu de lumière active, ce qui entraîne une bonne résolution spatiale.The dispersions according to the present invention also have a good depth of polymerization. This characteristic is an important factor for obtaining objects in stereophotolithography, because a too low polymerization depth does not allow satisfactory adhesion of the layers. Furthermore, due to their good transparency properties, the dispersions according to the invention diffuse little active light, which results in good spatial resolution.
Pour déterminer la profondeur de polymérisation, on place dans une cuve pour spectrophotomètre UV, de section 1 cm2, l'échantillon de la dispersion à tester contenant 1 % en poids d'IRGATURER 500 qui est un mélange équipondéral de benzophénone et d'hy- droxy-1 cyclohexylphénylcétone, puis l'échantillon est irradié ponctuellement avec un rayon laser pendant une durée déterminée (1 minute pour un laser d'une puissance de 100 mW). On vide ensuite la cuve, on lave à l'acétone le polymère obtenu, puis on mesure la hauteur du pic du polymère formé au point d'impact du rayon laser. Pour les différentes dispersions selon la présente invention, les hauteurs des pics mesurées varient de 4 à 7 mm, correspondant à une très bonne profondeur de polymérisation.To determine the depth of polymerization, a sample of the dispersion to be tested containing 1% by weight of IRGATURE R 500, which is an equal-weight mixture of benzophenone and, is placed in a tank for UV spectrophotometer, of section 1 cm 2 . 1-hydroxy-cyclohexylphenyl ketone, then the sample is punctually irradiated with a laser beam for a determined period (1 minute for a laser with a power of 100 mW). The tank is then emptied, the polymer obtained is washed with acetone, then the height of the peak of the polymer formed at the point of impact of the laser beam is measured. For the various dispersions according to the present invention, the heights of the peaks measured vary from 4 to 7 mm, corresponding to a very good depth of polymerization.
Les dispersions selon la présente invention présentent aussi une viscosité satisfaisante pour réaliser sans problème des objets de forme complexe en stéréophotolithographie.The dispersions according to the present invention also have a satisfactory viscosity for producing objects of complex shape in stereophotolithography without problem.
Les exemples suivants illustrent la présente invention sans toutefois la limiter.The following examples illustrate the present invention without, however, limiting it.
On mélange à la température ambiante, sous agitation, 8000 g d'un hydrosol de silice commercialisé sous le nom de KLEBOSOLR 1344 Na par la Société Française Hoechst présentant un pH de 9,7 et contenant pondéralement 69,6 % d'eau, 0,4 % de Na20 et 30 % de silice à l'état de particules monodisperses, non liées entre elles par des liaisons siloxane et présentant un diamètre moyen de 13 nm avec 708 g (0,9 I) d'une résine échangeuse de cations à groupements sulfoniques sous forme acide et d'une capacité d'échange de 2 eq/1. Après une heure d'agitation, la résine est séparée du milieu réactionnel par filtration. On obtient ainsi environ 8000g d'un hydrosol de silice acide présentant un pH = 2, et contenant pondéralement environ 70 % d'eau et 30 % de silice à l'état de particules monodisperses d'un diamètre moyen de 13 nm.8000 g of a silica hydrosol sold under the name of KLEBOSOL R 1344 Na by the French company Hoechst are mixed at ambient temperature, with stirring, having a pH of 9.7 and containing 69.6% by weight of water, 0.4% Na 2 0 and 30% silica in the form of monodisperse particles, not linked to each other by siloxane bonds and having an average diameter of 13 nm with 708 g (0.9 I) of a resin cation exchanger with sulfonic groups in acid form and with an exchange capacity of 2 eq / 1. After one hour of stirring, the resin is separated from the reaction medium by filtration. This gives approximately 8000 g of an acid silica hydrosol having a pH = 2, and containing approximately 70% water and 30% silica by weight in the form of monodisperse particles with an average diameter of 13 nm.
On mélange, sous agitation, à la température ambiante, 4130,2 g de l'hydrosol de silice acide préparé ci-dessus avec 851,3 g d'acrylate d'hydroxy-2 éthyle commercial et 17,2 g d'hydroquinone. Puis, l'eau présente dans le milieu réactionnel est distillée sous agitation, à une température inférieure à 55°C, sous une pression réduite progressivement de 60 à 20 mbar. On obtient ainsi 2110 g d'un organosol de silice contenant pondéralement 38,4 % d'acrylate d'hydroxy-2 éthyle, 0,6 % d'eau déterminée par la méthode de Karl Fischer, 0,8 % d'hydroquinone et 60,2 % de silice à l'état de particules discrètes, monodisperses, d'un diamètre moyen de 13 nm, non liées entre elles par des liaisons siloxane et présentant à 20°C, une densité de 1,576 et une viscosité Brookfield de 2200 mPa.s à 780 tours par minute.4130.2 g of the acid silica hydrosol prepared above are mixed, with stirring, at ambient temperature, with 851.3 g of commercial 2-hydroxyethyl acrylate and 17.2 g of hydroquinone. Then, the water present in the reaction medium is distilled with stirring, at a temperature below 55 ° C, under a pressure gradually reduced from 60 to 20 mbar. 2110 g of a silica organosol are thus obtained containing by weight 38.4% of 2-hydroxyethyl acrylate, 0.6% of water determined by the Karl Fischer method, 0.8% of hydroquinone and 60.2% silica in the form of discrete, monodisperse particles, with an average diameter of 13 nm, not linked to each other by siloxane bonds and having at 20 ° C, a density of 1.576 and a Brookfield viscosity of 2200 mPa.s at 780 rpm.
On prépare comme précédemment un hydrosol acide de silice, présentant un pH = 2,1 et contenant pondéralement 50 % d'eau et 50 % de silice à l'état de particules discrètes, monodisperses, d'un diamètre moyen de 50 nm, non liées entre elles par des liaisons siloxane, à partir d'un hydrosol de silice commercial stabilisé, présentant un pH de 9,3 et contenant pondéralement 50 % d'eau, 0,3 % de Na20 et 49,7 % de silice à l'état de particules monodisperses, d'un diamètre moyen de 50 nm, non liées entre elles par des liaisons siloxane.As before, a hydrosol acid silica is prepared, having a pH = 2.1 and containing by weight 50% water and 50% silica in the form of discrete, monodisperse particles, with an average diameter of 50 nm, not linked together by siloxane bonds, from a stabilized commercial silica hydrosol, having a pH of 9.3 and containing 50% by weight of water, 0.3% of Na 2 0 and 49.7% of silica in the form of monodisperse particles, with an average diameter of 50 nm, not linked to each other by siloxane bonds.
On mélange ensuite sous agitation et à la température ambiante, 2808,3 g de cet hydrosol acide de silice avec 611,4 g d'acrylate d'hydroxy-2 éthyle et 16,6 g d'hydroquinone. Puis l'eau présente dans le milieu réactionnel est éliminée par distillation, sous agitation, à une température inférieure à 55 °C, sous une pression réduite progressivement de 60 à 20 mbar. On obtient ainsi 2035 g d'une dispersion silico-acrylique contenant pondéralement 30,3 % d'acrylate d'hydroxy-2 éthyle, 0,8 % d'hydroquinone, 0,7 % d'eau et 68,2 % de silice à l'état de particules discrètes, monodisperses, d'un diamètre moyen de 50 nm, non liées entre elles par des liaisons siloxane, et présentant une viscosité Brookfield, déterminée à 20°C, sous 780 tours par minute de 8000 mPa.s.Then mixed with stirring and at room temperature, 2808.3 g of this silica acid hydrosol with 611.4 g of 2-hydroxyethyl acrylate and 16.6 g of hydroquinone. Then the water present in the reaction medium is removed by distillation, with stirring, at a temperature below 55 ° C, under a pressure gradually reduced from 60 to 20 mbar. 2035 g of a silicone-acrylic dispersion are thus obtained containing 30.3% by weight of acrylate of 2-hydroxyethyl, 0.8% of hydroquinone, 0.7% of water and 68.2% of silica in the form of discrete, monodisperse particles, with an average diameter of 50 nm, unbound between them by siloxane bonds, and having a Brookfield viscosity, determined at 20 ° C., at 780 rpm of 8000 mPa.s.
Cette dispersion silico-acrylique est ensuite diluée avec 100 g d'acrylate d'hydroxy-2 éthyle pour amener son titre en silice à 65 % en poids. On obtient ainsi une dispersion silico-acrylique présentant, à 20°C, une densité de 1,635 et une viscosité Brookfield de 740 mPa.s, sous 780 tours par minute et contenant pondéralement 33,5 % d'acrylate d'hy- droxy-2 éthyle, 0,7 % d'eau, 0,8 % d'hydroquinone et 65 % de silice à l'état de particules monodisperses d'un diamètre moyen de 50 nm, non liées entre elles par des liaisons siloxane.This silico-acrylic dispersion is then diluted with 100 g of 2-hydroxyethyl acrylate to bring its silica titer to 65% by weight. A silicone-acrylic dispersion is thus obtained having, at 20 ° C., a density of 1.635 and a Brookfield viscosity of 740 mPa.s, at 780 rpm and containing by weight 33.5% of hydroxy acrylate. 2 ethyl, 0.7% water, 0.8% hydroquinone and 65% silica in the form of monodisperse particles with an average diameter of 50 nm, not linked to each other by siloxane bonds.
On mélange sous agitation, à la température ambiante, 500 g de la dispersion silico-acrylique obtenue à l'exemple 1 et 500 g de la dispersion silico-acrylique obtenue à l'exemple 2. On obtient ainsi 1000 g d'une dispersion silico-acrylique contenant pondéralement 36 % d'acrylate d'hydroxy-2 éthyle, 0,7 % d'eau, 0,7 % d'hydroquinone et 62,5 % de silice à l'état de particules discrètes, polydisperses, non liées entre elles par des liaisons siloxane dont 48 % d'entre elles en poids, présentent un diamètre moyen de 13 nm et 52 % un diamètre moyen de 50 nm. Cette dispersion présente une densité de 1,605.500 g of the silica-acrylic dispersion obtained in Example 1 and 500 g of the silico-acrylic dispersion obtained in Example 2 are mixed with stirring at room temperature. 1000 g of a silico dispersion are thus obtained -acrylic containing 36% by weight of 2-hydroxyethyl acrylate, 0.7% of water, 0.7% of hydroquinone and 62.5% of silica in the form of discrete, polydisperse, unbound particles between them by siloxane bonds, 48% of which by weight, have an average diameter of 13 nm and 52% an average diameter of 50 nm. This dispersion has a density of 1.605.
On mélange sous agitation, à la température ambiante, 666,7 g de l'hydrosol acide de silice préparé à l'exemple 1 avec 200 g d'un mélange de monoester de l'acide acrylique avec le propanediol-1,2 contenant 75 % d'acrylate d'hydroxy-2 propyle, 25 % d'acrylate d'hydroxy-2 méthyl-1 éthyle et 33,4 g d'hydroquinone. Puis, l'eau présente dans ce milieu réactionnel est distillée, sous agitation, à une température inférieure à 55°C, sous une pression réduite progressivement de 60 à 20 mbar. On obtient ainsi 400 g d'une dispersion silico-acrylique contenant pondéralement 48 % de monoesters de l'acide acrylique avec le propanediol-1,2, 0,8 % d'hydroquinone, 0,8 % d'eau et 50 % de silice à l'état de particules monodisperses, d'un diamètre moyen de 13 nm, non liées entre elles par des liaisons siloxane et présentant à 20 °C, une densité de 1,446 et une viscosité Brookfield, à 780 tours par minute, de 1528 mPa.s.666.7 g of the silica acid hydrosol prepared in Example 1 are mixed with room temperature, with stirring, with 200 g of a mixture of acrylic acid monoester with 1,2-propanediol containing 75 % of 2-hydroxypropyl acrylate, 25% of 2-hydroxyethyl methyl-1 ethyl acrylate and 33.4 g of hydroquinone. Then, the water present in this reaction medium is distilled, with stirring, at a temperature below 55 ° C, under a pressure gradually reduced from 60 to 20 mbar. 400 g of a silico-acrylic dispersion are thus obtained, containing by weight 48% of monoesters of acrylic acid with propanediol-1,2, 0.8% of hydroquinone, 0.8% of water and 50% of silica in the state of monodisperse particles, with an average diameter of 13 nm, not linked to each other by siloxane bonds and having at 20 ° C, a density of 1.446 and a Brookfield viscosity, at 780 rpm, of 1528 mPa.s.
Dans la dispersion préparée à l'exemple 3, on introduit à la température ambiante, sous agitation, 1 % en poids de benzophénone et 1 % en poids d'hydroxy-1 cyclohexylphénylcétone, puis avec ce mélange, on prépare sur une machine de stéréophotolithographie équipée d'une source laser à argon ionisé fonctionnant dans l'ultraviolet (351 et 363 nm) un cube alvéolé de 30 mm d'arête contenant 36 alvéoles parallélépi- pèdiques, avec une grille de maille de 5 mm, avec une vitesse de déplacement du faisceau laser de 2,4 cm/s, une puissance de 400 mW et une épaisseur de couche de 0,25 mm. On obtient ainsi avant la post-polymérisation, un objet transparent, d'excellente présentation, avec des parois épaisses, régulières et bien définies. Après une post-polymérisation de 90 minutes dans une étuve à 150 °C, le cube alvéolé est totalement dur et il ne présente ni fissure, ni trace de silice en surface. Le retrait volumique est de 4 % (dp = 1,666).In the dispersion prepared in Example 3, 1% by weight of benzophenone and 1% by weight of 1-hydroxycyclohexylphenylketone are introduced at ambient temperature, with stirring, then with this mixture, preparation is carried out on a stereophotolithography machine equipped with an ionized argon laser source operating in the ultraviolet (351 and 363 nm) a honeycomb cube with 30 mm edge containing 36 parallelepepedic cells, with a mesh grid of 5 mm, with a speed of movement laser beam of 2.4 cm / s, a power of 400 mW and a layer thickness of 0.25 mm. Before the post-polymerization, there is thus obtained a transparent object, of excellent presentation, with thick, regular and well defined walls. After a 90-minute post-polymerization in an oven at 150 ° C, the honeycomb cube is completely hard and has no cracks or traces of silica on the surface. The volume shrinkage is 4% (dp = 1.666).
On prépare un cube alvéolé, comme dans l'exemple 5, avec les dispersions préparées dans les exemples 1 et 2 dans lesquelles on a introduit 1 % en poids de benzophénone et 1 % en poids d'hydroxy-1 cyclohexylphénylcétone. On obtient ainsi deux cubes alvéolés de présentation correcte, avec des parois transparentes et bien définies. Le retrait volumique est de 6 % pour la dispersion de l'exemple 1 et de 1,5 % pour la dispersion de l'exemple 2.A honeycomb cube is prepared, as in Example 5, with the dispersions prepared in Examples 1 and 2 into which 1% by weight of benzophenone and 1% by weight of 1-hydroxycyclohexylphenylketone have been introduced. This gives two honeycomb cubes of correct presentation, with transparent and well-defined walls. The volume shrinkage is 6% for the dispersion of Example 1 and 1.5% for the dispersion of Example 2.
Dans une dispersion commerciale de silice dans l'acrylate d'hydroxy-2 éthyle contenant pondéralement 69,2 % d'acrylate d'hydroxy-2 éthyle, 0,8 % d'eau et 30 % de silice à l'état de particules discrètes, monodisperses, d'un diamètre moyen de 13 nm, présentant une densité de 1,259, on prépare comme dans l'exemple 5 un cube alvéolé après introduction dans la dispersion de 1 % en poids de benzophénone et de 1 % en poids d'hydroxy-1 cyclohexylphénylcétone.In a commercial dispersion of silica in 2-hydroxyethyl acrylate containing by weight 69.2% of 2-hydroxyethyl acrylate, 0.8% of water and 30% of silica in the form of particles discrete, monodisperse, with an average diameter of 13 nm, having a density of 1.259, a honeycomb cube is prepared as in Example 5 after introduction into the dispersion of 1% by weight of benzophenone and 1% by weight of 1-hydroxy cyclohexylphenyl ketone.
On obtient ainsi un cube de très mauvaise présentation avec des parois boursouflées et une mauvaise adhérence entre les couches. Le retrait volumique de cette dispersion est de 15 %.This gives a cube of very poor presentation with puffy walls and poor adhesion between the layers. The volume shrinkage of this dispersion is 15%.
Claims (10)
dans laquelle soit R et R1' identiques, représentent un atome d'hydrogène, soit R et Ri, différents, représentent un atome d'hydrogène ou un radical méthyle, caractérisées par le fait qu'elles contiennent pondéralement de 50 à 70% de silice à l'état de particules discrètes, polydisperses, non liées entre elles par des liaisons siloxane d'un diamètre moyen compris entre 10 et 50 nm.1. Dispersions of colloidal silica in an alkanol acrylate or a mixture of alkanol acrylates of general formula (I)
in which either R and R 1 ′ are identical, represent a hydrogen atom, or R and R i , which are different, represent a hydrogen atom or a methyl radical, characterized in that they contain 50 to 70% by weight of silica in the form of discrete, polydisperse particles, not linked together by siloxane bonds with an average diameter of between 10 and 50 nm.
dans laquelle soit R et R1' identiques, représentent un atome d'hydrogène, soit R et R1' différents, représentent un atome d'hydrogène ou un radical méthyle, de manière à obtenir le taux de silice désiré compris entre 50 et 70 % en poids, puis que l'on distille l'eau présente dans cette dispersion, sous agitation, à une température inférieure à 55 °C, et sous pression réduite, jusqu'à un taux d'eau résiduelle inférieur à 1 % en poids, déterminé par la méthode de Karl Fischer, pour obtenir une dispersion monodisperse de silice colloïdale dans l'acrylate d'alcanol ou le mélange d'acrylates d'alcanols de formule générale (I) choisi, contenant de 50 à 70 % en poids de silice sous forme de particules discrètes non liées entre elles par des liaisons siloxane, présentant un diamètre moyen de 10 à 50 nm que l'on mélange, à la température ambiante, dans des proportions convenables, avec une ou plusieurs autres dispersions monodisperses de silice colloïdale de granulométrie souhaitée et de taux en silice adéquat, dans un acrylate d'alcanol ou un mélange d'acrylates d'alcanols de formule générale (I) identique et préparées selon le procédé décrit ci-dessus, de manière à obtenir la dispersion silico- acrylique polydisperse souhaitée.4. Process for the preparation of the dispersions according to any one of claims 1 to 3, characterized in that a silica hydrosol, monodisperse, in acid form, containing 30 by weight, is mixed, with stirring. with 50% silica in the form of discrete particles not linked to each other by siloxane bonds, with an average diameter of 10 to 50 nm with a calculated amount of an alkanol acrylate, or of a mixture of alkanol acrylates of general formula (I)
in which either R and R 1 ′ are identical, represent a hydrogen atom, or R and R 1 ′ different, represent a hydrogen atom or a methyl radical, so as to obtain the desired silica content of between 50 and 70 % by weight, then the water present in this dispersion is distilled, with stirring, at a temperature below 55 ° C, and under reduced pressure, to a residual water content of less than 1% by weight , determined by the Karl Fischer method, to obtain a monodisperse dispersion of colloidal silica in the alkanol acrylate or the mixture of alkanol acrylates of general formula (I) chosen, containing from 50 to 70% by weight of silica in the form of discrete particles not linked to each other by siloxane bonds, having an average diameter of 10 to 50 nm which are mixed, at room temperature, in suitable proportions, with one or more other monodisperse dispersions of colloidal silica e of desired particle size and adequate silica content, in an alkanol acrylate or a mixture of alkanol acrylates of identical general formula (I) and prepared according to the process described above, so as to obtain the silico dispersion - desired polydisperse acrylic.
dans laquelle soit R et R1' identiques, représentent un atome d'hydrogène, soit R et Ri, différents, représentent un atome d'hydrogène ou un radical méthyle, caractérisées par le fait qu'elles contiennent pondéralement de 50 à 70% de silice à l'état de particules discrètes, non liées entre elles par des liaisons siloxane d'un diamètre moyen compris entre 10 et 50 nm.7. Use in stereophotolithography, as resin, dispersions of colloidal silica in an alkanol acrylate and a mixture of alkanol acrylates of general formula (I)
in which either R and R 1 ' identical, represent a hydrogen atom, or R and R i , different, represent a hydrogen atom or a methyl radical, characterized in that they contain 50% to 70% by weight of silica in the form of discrete particles, not linked to one another by siloxane bonds with an average diameter of between 10 and 50 nm.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR9204297 | 1992-04-08 | ||
FR9204297A FR2689876B1 (en) | 1992-04-08 | 1992-04-08 | Silico-acrylic dispersions, their production process, their application in stereophotolithography and process for the preparation of resin objects. |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0565403A1 true EP0565403A1 (en) | 1993-10-13 |
EP0565403B1 EP0565403B1 (en) | 1997-10-08 |
Family
ID=9428633
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19930400805 Expired - Lifetime EP0565403B1 (en) | 1992-04-08 | 1993-03-29 | Silica/acrylation dispersions, method for producing them, their use in stereophotolithography and method for preparing articles made of resin |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP0565403B1 (en) |
CA (1) | CA2092244A1 (en) |
DE (1) | DE69314374T2 (en) |
DK (1) | DK0565403T3 (en) |
FR (1) | FR2689876B1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2772777A1 (en) * | 1997-12-23 | 1999-06-25 | Clariant Chimie Sa | SILICO-ACRYLIC COMPOSITIONS, PREPARATION METHOD AND APPLICATION FOR OBTAINING THERMALLY OR RADIATION CURABLE COATINGS |
FR2781922A1 (en) * | 1998-07-31 | 2000-02-04 | Clariant France Sa | METHOD FOR THE MECHANICAL CHEMICAL POLISHING OF A LAYER OF A COPPER-BASED MATERIAL |
US6025114A (en) * | 1995-03-11 | 2000-02-15 | Zeneca Limited | Liquid photocurable compositions |
EP1236765A1 (en) * | 2001-02-28 | 2002-09-04 | hanse chemie GmbH | Silica dispersion |
EP1508834A2 (en) * | 2003-08-19 | 2005-02-23 | 3D Systems, Inc. | Nanoparticle-filled stereolithographic resins |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19617931C5 (en) * | 1996-04-26 | 2010-07-22 | Ivoclar Vivadent Ag | Use of a filled and polymerizable material as dental material |
AU3505400A (en) † | 1999-10-28 | 2001-05-08 | 3M Innovative Properties Company | Dental materials with nano-sized silica particles |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0220026A2 (en) * | 1985-10-18 | 1987-04-29 | Sumitomo Chemical Company, Limited | Silica or alumina sol using reactive monomer as dispersion medium |
EP0393673A2 (en) * | 1989-04-21 | 1990-10-24 | E.I. Du Pont De Nemours And Company | Solid imaging method using multiphasic photohardenable compositions |
EP0460560A2 (en) * | 1990-06-04 | 1991-12-11 | Kawasaki Steel Corporation | Polymerizable silica sol, adamantane derivative for use in the sol and cured resin prepared using the same |
-
1992
- 1992-04-08 FR FR9204297A patent/FR2689876B1/en not_active Expired - Fee Related
-
1993
- 1993-03-23 CA CA 2092244 patent/CA2092244A1/en not_active Abandoned
- 1993-03-29 DK DK93400805T patent/DK0565403T3/en active
- 1993-03-29 DE DE1993614374 patent/DE69314374T2/en not_active Expired - Fee Related
- 1993-03-29 EP EP19930400805 patent/EP0565403B1/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0220026A2 (en) * | 1985-10-18 | 1987-04-29 | Sumitomo Chemical Company, Limited | Silica or alumina sol using reactive monomer as dispersion medium |
EP0393673A2 (en) * | 1989-04-21 | 1990-10-24 | E.I. Du Pont De Nemours And Company | Solid imaging method using multiphasic photohardenable compositions |
EP0460560A2 (en) * | 1990-06-04 | 1991-12-11 | Kawasaki Steel Corporation | Polymerizable silica sol, adamantane derivative for use in the sol and cured resin prepared using the same |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6025114A (en) * | 1995-03-11 | 2000-02-15 | Zeneca Limited | Liquid photocurable compositions |
FR2772777A1 (en) * | 1997-12-23 | 1999-06-25 | Clariant Chimie Sa | SILICO-ACRYLIC COMPOSITIONS, PREPARATION METHOD AND APPLICATION FOR OBTAINING THERMALLY OR RADIATION CURABLE COATINGS |
EP0926170A1 (en) * | 1997-12-23 | 1999-06-30 | Clariant (France) S.A. | Silico-acrylic compositions, process of preparation and use as coatings which can be hardened either thermally or by irradiation |
US6136912A (en) * | 1997-12-23 | 2000-10-24 | Clariant (France) S.A. | Silicoacrylic compositions, preparation process and use for obtaining coatings which are hardenable thermally or by radiation |
FR2781922A1 (en) * | 1998-07-31 | 2000-02-04 | Clariant France Sa | METHOD FOR THE MECHANICAL CHEMICAL POLISHING OF A LAYER OF A COPPER-BASED MATERIAL |
EP0982766A1 (en) * | 1998-07-31 | 2000-03-01 | Clariant (France) S.A. | Process for chemo-mechanical polishing of a copper-based material layer |
US6302765B1 (en) | 1998-07-31 | 2001-10-16 | Clariant France S.A. | Process for mechanical chemical polishing of a layer in a copper-based material |
EP1236765A1 (en) * | 2001-02-28 | 2002-09-04 | hanse chemie GmbH | Silica dispersion |
WO2002083776A1 (en) * | 2001-02-28 | 2002-10-24 | Hanse Chemie Ag | Silicon dioxide dispersion |
EP1508834A2 (en) * | 2003-08-19 | 2005-02-23 | 3D Systems, Inc. | Nanoparticle-filled stereolithographic resins |
EP1508834A3 (en) * | 2003-08-19 | 2006-05-17 | 3D Systems, Inc. | Nanoparticle-filled stereolithographic resins |
Also Published As
Publication number | Publication date |
---|---|
EP0565403B1 (en) | 1997-10-08 |
DE69314374D1 (en) | 1997-11-13 |
DE69314374T2 (en) | 1998-03-05 |
DK0565403T3 (en) | 1997-10-27 |
CA2092244A1 (en) | 1993-10-09 |
FR2689876B1 (en) | 1994-09-02 |
FR2689876A1 (en) | 1993-10-15 |
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